Production of Ethanol From Corn Crops September 28, Homwork #1 ChE – Senior Design I Instructor: Dr. Betul Bilgin Group 5, Tu/Th AM Section Waseem Jaban Arun Joseph Kevin Wu Patrick Yau Department of Chemical Engineering University of Illinois at Chicago TABLE OF CONTENTS Project Charter………………………………………………………….……………………….2 Design Plan……..…………………………………………………………………………..…….3 Introduction……………………………………………………..…………………..………… Objective……………………………………………………………………………… Market Analysis……………………………………………………..……………… Process Description Problem………………………………………………………………………………… Possible Solutions……………………………………………………………………… Chosen Solution………………………………………………………………………… Design Basis………………………………………………………….……………… Operating Conditions, Flow rates, and Assumptions……………….………………… Material Balance…………………………………………………………………………24 BFD…………………………………………………………………………….…… PFD…………………………………………………………………………………… Equipment Description……………………………………………………………… References/Bibliography………………………………………………………………… Page 1 Department of Chemical Engineering University of Illinois at Chicago PROJECT CHARTER OPPORTUNITY The design team’s chemical process synthesis of ethanol through fermentation of corn meets criteria for economical and effective design GOAL Introduce and simultaneously optimize the process of ethanol production through esterification to fit customer specifications OBJECTIVES ● Find a environmentally friendly way to produce ethanol ● Produce ethanol at a high industrial/fuel grade purity for industrial use IN SCOPE ● Designing the process of dry-mill fermentation of corn to produce ethanol ● Comparison and optimization of multiple processes facilitation the production of ethanol CORE TEAM MEMBERS ROLE Waseem Jaban: Design team leader Arun Joseph: Design team member Kevin Wu: Design team member Patrick Yau: Design team member PROJECT STATUS SUMMARY Project Start Date: 9/22/17 Estimated Completion: 9/28/17 Completion Date: 9/27/17 Process Impacted: Ethanol production MILESTONES Project assigned: 9/14/17 Design plan approval: 9/22/17 Literature review and market analysis: 9/23/17 Indirect hydrolysis process selection: 9/26/17 BDF and PDF production: 9/27/17 Submission of project: 9/28/17 OUT OF SCOPE ● Developing waste stream into revenue stream ● Safety considerations ● EPA compliance ASSUMPTIONS ● Reaction conditions ● Unlimited budget ● Process will be running a dry mill hydration of ethanol DELIVERABLES ● Market analysis of ethanol as of 28 September ● Potential ethanol production methods and alternatives ● Block flow diagram and process flow diagram of our chosen fermentation design DESIGN PLAN Page 2 Department of Chemical Engineering University of Illinois at Chicago INTRODUCTION Page 3 Department of Chemical Engineering University of Illinois at Chicago Objective Chosen by our consulting company to design and prepare an introductory report of the chemical synthesis of ethanol, the purpose of our report is to summarize our final design and extrapolate our results for potential future applications. Ethanol is a grain alcohol utilized for a plethora of processes: medical applications, chemical solvent, synthesis of other compounds, and even a clean energy fuel source. However, the largest single use of ethanol is as an engine fuel and fuel additive. In , U.S. fuel ethanol production soared to more than billion gallons. According to Figure 1, the U.S. is the world’s largest producer of ethanol; with Brazil far behind at second, both countries combined produce close to 85% of the world ethanol production . Such long development in production forces us to ponder, why such an increase all of a sudden? Figure 1: Global Ethanol Production  As reported by the U.S. Environmental Protection Agency (EPA) in Figure 2, for the EPA requirements for conventional renewable fuel blending are finally meeting statutory levels. With the desire for more octane content in gasoline, gasoline refiners have steered away from Page 4 Department of Chemical Engineering University of Illinois at Chicago producing octane from hydrocarbons to “take advantage of ethanol’s superior clean octane properties”. The addition of ethanol to gasoline not only reduces knocking in vehicle engines, but also cuts down on tailpipe emissions of exhaust hydrocarbons, carcinogens like benzene, carbon monoxide, many greenhouse gases, and small particles in the air which may cause complications in the respiratory system if ingested. Ethanol recycling of atmospheric carbon has reduced greenhouse gas emissions enough in the past year to equate to taking million cars off the road for an entire year. By focusing more efforts on producing octane through ethanol, refiners have not only found a more cost and energy efficient source of octane, but have also shaped the future of fuel consumption. Automakers are encouraged to produce vehicles which require more fuel efficient ethanol blends which in turn has resulted in the increasing presence of retail stations across the nation offering various blends of ethanol called flex fuels ( Ethanol Industry,2, 12, 14, 16, 18, 28, 29). Figure 2: RFS Conventional Renewable Fuel Volume Requirements  However, according to EPA data, auto- manufacturers are slowing down their production of flex fuel vehicles due to the down-scaled Page 5 Department of Chemical Engineering University of Illinois at Chicago fuel economy credits. Fuel economy credit is a miles per gallon credit manufacturers receive from the government for producing vehicles which have high Corporate Average Fuel Economy (CAFE) ratings (high fuel efficiency). In an attempt to push sales of such vehicles, the government multiplies the sale of the vehicles by a certain factor. As reported by EPA, the factor for electric vehicle sales will scale down from to by . Beyond being utilized for octane production, the process of producing dry-grind ethanol from corn has several other benefits including the various uses for its co-products. One example is the use of Distiller’s Dried Grains with Solubles (DDGS) for conducting electricity . As a continuously growing sector, efficient design of ethanol production relying on corn crops is increasingly vital. Observations of these trends are outlined in our market analysis of dfknj.wz.cz process of ethanol production from corn can be broken down into two main categories; dry grind and wet mill. While dry mill co-products become DDGS and corn distillers oil, wet mill coproducts include corn germ components such fiber, starch, and even gluten which is utilized as animal feed . Though wet milling produces a higher yield of ethanol per corn bushel as well as a larger variety of products, the capital costs involved in dry milling are significantly less than those present in the wet milling process . As exemplified by statistics gathered by the U.S. Department of Agriculture in Figure 3, the vast majority of U.S. ethanol production is facilitated using the dry mill process which is why we structured our design off of the dry-mill fermentation of corn to produce ethanol . Further optimization and identification of problems within our chosen design process thereby impacts multiple industries. Figure 3: U.S. Grain Ethanol Production by Technology Type Page 6 Department of Chemical Engineering University of Illinois at Chicago Market Analysis: According to the U.S Energy Information Administration (EIA), ethanol production reached billion gallons, and although there are no current data for the years of and , a study done by Patricia Batres-Marquez who works at , shows that the ethanol production for the year of and are billion gallons, and billion gallons, respectively. Figure 4: Ethanol Production in the U.S. and Selected States in Billion Gallons Page 7 Department of Chemical Engineering University of Illinois at Chicago According to the latest data collected by EIA, in , the production of ethanol in the U.S was 59 thousands barrels per day, with a consumption rate fairly close to the amount produced. Figure 5: Annual U.S. Ethanol Production and Consumption EIA’s data which was analyzed by Marquez indicate that the U.S monthly consumption averaged to million gallons per day in the year of , which is equivalent to billion gallons per year. Figure 6: U.S. Annual Gasoline Consumption and Estimated Ethanol Consumption Blended into Motor Gasoline Page 8 Department of Chemical Engineering University of Illinois at Chicago The production outlook for according to EIA’s data analyzed by Marquez shows the production of ethanol will increase to million gallons per day. The data also suggests that the amount of ethanol that is going to be used in motor gasoline will be approximately million gallons per day, making it the number one consumption factor. However, the production rate exceeds the consumption rate, which will lead to the need to export the excess ethanol to other countries. The ethanol export rate will have to be around million gallons per day. There are two main factors that affect the ethanol price market: oil prices and feed grains. Oil prices affect the price of ethanol simply because of the alcohol fuel’s major contribution in gasoline blending. However, the price of ethanol is also determined by the price of feed grains such as corn which serves to be the most readily available raw material necessary for the production of the commodity. A study was done by Dr. Dan O’Brien and Dr. Mike Woolverton from Kansas State University in the AgMRC Renewable Fuels Newsletter shows clearly how Iowa ethanol prices is related directly to oil prices. Page 9 Department of Chemical Engineering University of Illinois at Chicago Figure 7: Iowa Ethanol and Midwest Gasoline Prices Furthermore, the chart below shows clearly how the three (oil, corn, and ethanol prices) are closely related. Also, According to Dr. Dan O’Brien and Dr. Mike Woolverton “ Corn processing for ethanol is second in size only to the domestic livestock feed market and may become the largest source of demand in three years.” Figure 8: Index of Monthly Crude Oil, Gasoline, Corn, and Ethanol Prices One of the biggest ethanol producing companies in Illinois and in the U.S is Marquis Energy, LLC. The company produces one million gallons of fuel grade ethanol per day, and well over million gallons of ethanol a year. Therefore, we will design our plant to produce million gallons of ethanol per year. The location of the plant is important. It should be close to a large Page 10 Department of Chemical Engineering University of Illinois at Chicago supply of corn like a corn farm, and have access to rail tracks for easy shipment, and/or a nearby interstate highway. Therefore, the ideal location for a plant seems to be in the midwest, where corn crops and water are abundant. It would also be most efficient to have a plant located near a shipping railroad track so the transportation process can be as smooth as possible. The image below shows Marquis Energy plant. The train track lies in the top portion of the image, while the highway (Not shown in the image) lies on the opposite side. Figure 9: Aerial View of the Marquis Energy Plant in Putnam, Illinois (Google Earth) Page 11 Department of Chemical Engineering University of Illinois at Chicago PROCESS DESCRIPTION Problem For fermentation, the reaction that governs this process is the conversion of glucose to ethanol and carbon dioxide byproduct. C6 H 12 O6 →2 C 2 H 5 OH +2 C O2 Now we need a source of this glucose in order to arrive at our product. With fermentation we use biological materials such as corn, sugarcane and other plants containing starch or sugar. Because of our central location and proximity to corn fields we will use corn as our starting material for our ethanol process. When delivered the whole corn cobs are sorted to remove debris and then milled into corn starch, similar to what is at the supermarket.  After being grounded into flour, the starch is then mixed with water and a enzyme (alpha-amylase) and heated to reduce the viscosity of the mixture.  The slurry is now at the liquefaction stage, where the solid portion of the mix is now turned into pure liquid. The slurry is introduced into a pressurized cooker and then heated at °C for a short time and then cooled.  The mixture is again heated for hours.  During this time the enzyme added before will now breakdown the starch into dextrins, glucose polymer chains. Page 12 Department of Chemical Engineering University of Illinois at Chicago  After this, another enzyme is added, glucoamylase which decomposes the dextrins into single pieces of glucose ready for the fermentation reaction above.  With the ethanol we want to produce, we intend to sell it to petroleum companies such as BP, Shell and Exxonmobil as an additive in their gasoline. With our product, it provides a home grown solution to produce environmentally friendly gas for American consumers. For gasoline made for the US market, two types of gasoline use ethanol as an additive, E10 and E E10 is comprised of 10% ethanol and 90% gas and E85 has a composition of 85% ethanol and 15% regular fuel . For our customers they will need a fairly pure product in order to ensure these ratios in their gasoline, so our final ethanol composition will be 99%. Possible Solution There are many ways to produce ethanol, for varying concentrations and uses, for instance, in synthetic ways such as using ethylene to directly synthesize ethanol through a catalyst. In addition, we can ferment sugar to create it as well in a very similar way beer and spirits are produced. This method is very versatile as the source materials can be anything from corn or sugarcane as the only requirement is that they have glucose within. A solution that can be used is the direct hydration of ethylene to ethanol. Water is introduced to vapor ethylene at an environment of ॰C and 70 bar in the presence of a catalyst of phosphoric acid and silica.  C H 2=C H 2 + H 2 O→ C2 H 5 OH Page 13 Department of Chemical Engineering University of Illinois at Chicago Afterwards, the reaction mixture is entrained in benzene in order to separate the product from excess water.  The advantages of this process is that the byproducts made are in very limited quantities, the selectivity of ethanol is 97%.  However, the conversion is very low, around 4%.  With such low production, in order to make this pathway usable ethylene must be recycled over and over and must be introduced at high concentration, which ramps up the costs.  Because of the reaction conditions needed, ॰C and 70 bar, an enormous amount of energy is required, this has to be taken from an outside utility that we pay for. Furthermore, catalyst is continuously lost during operation. Of course, this has to be replaced, shutting down the reactor and putting the plant on idle. Another industrial process to produce ethanol is indirect hydration in a manner very similar to direct hydration. Ethylene is reacted with highly concentrated sulfuric acid with Ag2SO4 as a catalyst, causing an ester to be produced. This method of manufacturing of ethanol involves two unit processes: absorption and hydrolysis. The concentration of the ethylene gases range from 35% to 95% reacting with % sulfuric acid:  C H 2=C H 2 + H 2 S O 4 → C 2 H 5 O−S O3 H C 2 H 5 O¿ 2 S O 2 C H 2=C H 2 +C 2 H 5 O−S O3 H → ¿ The first reaction produces ethyl hydrogen sulphate, and the second reaction produces diethyl sulphate. Diethyl sulfate C2 H 5 O ¿2 S O2 ¿ is highly toxic and a likely carcinogen and proves to be a substantial obstacle towards the use of this particular process.  Dilution of the resulting solution of sulfuric acid and diethyl sulfate with water allows the ester to hydrolyze to ethanol.  While this process has a very high conversion (85 %) , it suffers from many expensive Page 14 Department of Chemical Engineering University of Illinois at Chicago drawbacks that has limit its use in industry. In particular, the sulfuric acid is at such a high concentration (%) that it corrodes machinery and pipes from its insane acidity.  The continued cost of replacing corroded pipes and equipment would accumulate significantly over the lifespan of a plant. Furthermore, as a way of cost saving excess sulfuric acid is recycled from the end of the process. However, this involves re-concentrating the acid. The easiest way to do this is to heat the acid to boil off water, but a byproduct of this heating is that sulfur dioxide is made, which is toxic and must be dealt with.  Another byproduct of this reaction is diethyl ether, which is also a hazardous material as well as very volatile and poses safety concerns during operation.  C 2 H 5 ¿2 O C2 H 5 O ¿2 S O2 + H 2 O→ C2 H 5 OH +¿ ¿ C 2 H 5 ¿2 O C2 H 5 O−S O3 H + H 2 O →C 2 H 5 OH + ¿ What both of the discussed processes depend on for their viability is the cost of ethylene, which varies due to market fluctuations.  While the price depends on demand the main factor is the cost to produce ethylene. The chemical is made through the cracking of hydrocarbons, therefore the price of ethylene is dependent on the price of hydrocarbon sources such as natural gas and crude oil.  As we know when we fill up our cars, the price of gasoline (and oil) has been on the rise for the past years, thus processes such as the two outlined have fallen to the wayside. Figure Ethylene price trend (Duncan Seddon & Associates PTY. LTD.) Page 15 Department of Chemical Engineering University of Illinois at Chicago With the obsolescence of ethylene to ethanol processes, companies have turn to other ways of producing the needed commodity. In specific we turn to bioprocesses such as fermentation of simple sugars to produce ethyl alcohol. Fermentation relies on the conversion of glucose into ethanol and CO2, using yeast as a natural catalyst to perform this reaction. C6 H 12 O6 →2 C 2 H 5 OH +2 C O2 There are two variants of this process, dry mill and wet mill processing. The main difference between these two pathways is the way the glucose is refined from the source material. Dry mill production involves the preliminary grinding of the starting material (such as corn) into a starch, this is then mixed with water and enzymes that eventually creates glucose.  Wet mill processing differs where by the corn is first bathed in hot water to release all of the starch and then grinded into a pulp.  Afterwards the resulting mixture is separated into 3 parts: fiber, gluten and starch. The starch is then used to make the ethanol. Meanwhile, the fiber and gluten are furthered refined to make separate products that can be sold to further profit.  Page 16 Department of Chemical Engineering University of Illinois at Chicago In both these two processes the fermentation steps are similar. After the corn is broken down into starch it is mixed with water and a enzyme (alpha-amylase) and heated, during this time the enzyme breakdowns the starch into dextrins.  A further process is done where another enzyme is introduced (glucoamylase), this further tears down the dextrins into glucose molecules.  Once at this stage, the mix is pumped into fermentation tanks and yeast added and left to sit for hours.  The yeast acts as the catalyst for the reaction, at the end of the duration ethanol and carbon dioxide have replaced the glucose. Once this is finished the ethanol is distilled, separated and stored for sale. When compared to wet mill, dry mill processing is a cheaper solution for ethanol fermentation. This is due to the fact that the wet mill process is more cost intensive compared to the dry mill.  These associated costs go toward making the byproducts of the corn, the gluten and corn germ into marketable products for consumers such as livestock feed and corn oil.  Meanwhile, the dry mill process is tailored to exclusively producing ethanol and the solid byproduct Dried Distillers Grains (DDG) is also sold as feed product as well.  While the dry mill lends to higher ethanol production and lower capital expenses, the wet mill process is more versatile.  If ethanol prices were to plummet a wet mill plant can still weather the low off the sales of their byproducts, while a dry mill plant might have to shut down or lay off workers due to a downturn. Chosen Solution The challenges of producing ethanol from corn crops are the following steps: 1) Grinding. 2) Cooking and liquefaction. Page 17 Department of Chemical Engineering University of Illinois at Chicago 3) Saccharification. 4) Fermentation. 5) Distillation Figure Overview of a Dry Mill Plant Page 18 Department of Chemical Engineering University of Illinois at Chicago Grinding can be done using two different methods, Dry Method, and Wet Method. These two methods will produce two different products. Dry milling which is the simpler process will produce ethanol, CO2, and dried distiller grain with solubles (DDGS). Wet milling will produce feed, corn oil, gluten meal and gluten feed. The most efficient and simple method is the dry milling that will be adopted for this process. It consist of using a hammer mill, or roller mill to grind the corn. The following photo shows how the corn get milled prior to cooking and liquefaction. Figure Illustration of a Hammer mill Page 19 Department of Chemical Engineering University of Illinois at Chicago The cooking stage of the grinded corn, which is referred to as gelatinization. It involved mixing the corn with water at temperatures higher than 60 degree Celsius, pH of range of , where ammonia and sulfuric acid are added to maintain the pH level. The process is partially hydrolysis that lowers the viscosity of the mixture. It is essentially breaking up the longer starch chains into smaller chains.  The liquefaction can be done with three similar options. The jet cooker process is chosen for this design, because the most efficient process. The image below describe the three processes. Figure Liquefaction process diagram Page 20 Department of Chemical Engineering University of Illinois at Chicago The common material that is added to the three processes is α-amylase. The α-amylase for liquefaction acts on the internal α (1,4) glycosidic bonds to yield dextrins and maltose (glucose dimers). Glucose is used in the next step to make ethanol. Now that glucose is present, the saccharification process to making ethanol can begin. The optimum conditions for the process are pH, and a temperature of degree Celsius. The glucose will further hydrolysis to glucose monomers, which are then fermented to produce ethanol and carbon dioxide. The following chemical reaction equation shows that one mole of glucose is converted to two moles of ethanol and carbon dioxide. C6H12O6→2C2H6OH + 2CO2 The reaction takes place in a batch reactor over 2 to 3 days at a temperature of 30 degree celsius. The conversion rate is between %. To initiate the reaction, yeast is added. The most common yeast is saccharomyces cerevisiae.  Page 21 Department of Chemical Engineering University of Illinois at Chicago The distillation is the last step of this process. The concentration of the ethanol in the mixture is about 15%. The other 85% is water. Water boils at degree Celsius, while ethanol boils at 78 degree celsius. One of the challenges faced when running the mixture in a distillation column to separate the two components is the fact that water and ethanol evaporate at a relatively lower temperature, and therefore, the distillate at the top of the column will contain 95% ethanol and 5% water.  To achieve a concentration of % ethanol, the method of dehydration is used. The unit that is used is called a molecular sieve, and the material used in it is called zeolite. The pore size of the zeolite membrane is nm, while the size of the water molecule is nm and the ethanol nm. Therefore, when the mixture is passed through these sieves at high and low pressure, the water molecules will pass through the Zeolite sieves, and ethanol molecules will be isolated.  Figure Ethanol Filtration Using Sieves (BEEMS Module B5) Page 22 Department of Chemical Engineering University of Illinois at Chicago Design Basis The estimated production of ethanol from corns are the followings; One bushel of corn (56 lbs.) will produce gal of ethanol, 17 lbs of CO2, and 17 lbs of DDGS (Distillers Dried Grains with Solubles). Bushel of corn: 56 lbs x 62% starch = lbs of starch lbs starch x lbs glucose/lb starch = lbs glucose/bu The reaction of glucose to ethanol C6H12O6→2C2H5OH + CO2 g/mol 2*46 g/mol lbs glucose x 92 lbs EtOH/ lbs glucose = lbs EtOH/bu lbs EtOH x 1 gal EtOH/ lbs = gal EtOH theoretically x (/) = 93% yield of ethanol Page 23 Department of Chemical Engineering University of Illinois at Chicago Operating Conditions, Flow rates, and Assumptions ● The corn particle size pass the mill is (<2 mm) to facilitate the subsequent penetration of water. ● The slurry tank’s pressure and temperature are 4 bar, °C, respectively. ● The liquefaction step will operate at 85 degree celsius. ● The fermentation reactor will convert % or raw materials to products. ● The first two distillation columns will operate under the pressure of and bar with a distillate products of 50% ethanol. ● The last distillation column will operate under pressure 5 bar with 92% w/ ethanol purity in the distillate. ● Specifications for all columns in distillation section of process are set to recover more than % of ethanol in the feed streams. Page 24 Department of Chemical Engineering University of Illinois at Chicago Material Balance The following process shows the overall steps: million gallons of ethanol need to be produced everyday to meet the goal of ~ million gallons produced in one year x10^6 gal of ethanol x (1 bushel of corn)/ gal of ethanol x 56 lbs corn = 22x10^6 lbs Corn x10^6 gal of ethanol/24 hours) x lbs/gallon = lbs/hour of ethanol Therefore, 22x10^6 lbs of corn is needed to produce ethanol at a rate of , lbs/hour in order to reach our production goal Figure Material Balance Calculations Page 25 Department of Chemical Engineering University of Illinois at Chicago The composition of corn is the following : Figure Corn Composition Component Mass fraction Water Xilose Starch Hemicellulose Cellulose Lignin Based on the above, the following flow rates were calculated: Figure Component Flow Rates BFD Page 26 Department of Chemical Engineering University of Illinois at Chicago The production of ethanol and related processes are in blue; the byproducts of distillation is sent to a centrifuge and process through the systems in grey. This byproduct is non-fermentable material and also known as whole stillage, consisting of suspended grain solids, dissolved materials, and water. The main byproducts produced are Wet Distillers Grains (WDG) which contains unfermented grain residues. WDGS indicates Wet Distillers Grains with Solubles. WDGS, upon drying, creates Distiller’s Dried Grains with Solubles suitable for animal feed and electricity production . Further analysis of this process and reutilization of this waste stream for revenue is out of scope for this report. Page 27 Department of Chemical Engineering University of Illinois at Chicago Process Flow Diagram Equipment and Process Description Page 28 Department of Chemical Engineering University of Illinois at Chicago Milling Process (Red Section) 1: Hammer Mill Mills aggregate material into smaller pieces. Corn is milled to < 2 mm in order to facilitate the mixing process with water in the mixer. Dry milling produces ethanol, CO2, and dried distiller grain with solubles (DDGS). 2: Mixer Water is added into the finely ground corn to saturate the material. Also receives recycled water from the fermentation process. Cooking Process (Orange Section) 3: Slurry Tank Receives slurry from mixer as well as ammonia and sulfuric acid to maintain pH level. 4: Jet Cooker The jet cooker utilizes steam to raise the temperature to oC and 4 bar. This sterilizes the slurry and breaks the hydrogen bonds to facilitate water absorption. Also known as gelatinization as the mixture becomes gelatinous. 5: Vacuum Flash Heats slurry to optimize yield, conversion, and avoidance of intractable products. Liquefaction (Yellow Section) 6: Liquefaction Tank At 85oC, alpha-amylase enzymes are added to the starch molecules at % dry basis with respect to corn. This decreases viscosity as alpha-1,4 glucosidic amylose and amylopectin linkages are broken. Simultaneous Saccharification and Fermentation (Green Section) Page 29 Department of Chemical Engineering University of Illinois at Chicago 7: Saccharification Tank Starch oligosaccharides are hydrolysed at a rate of 99% into glucose molecules by glucoamylase enzyme. This enzyme is added at % dry basis with respect to corn. 8: Mash steam cooler Mash resulting from liquefaction and saccharification are cooled to 35oC to facilitate propagation. 9: Yeast Starter Tank (Propagation) Yeast, or Saccharomices cerevistae, catalyzes glucose at a conversion rate of % within this tank. The remaining .5% is transformed by reaction. Fermentation Batch Reactor Glucose is converted to ethanol and carbon dioxide. This reaction occurs in batch reactor over two to three days at a temperature of 30oC. Outlet stream from fermenter is beer: contains negligible quantities of acetaldehyde, methanol, butanol, and small quantities of acetic acid, and glycerol. Absorption Column A large quantity of CO2 is produced as a consequence of the reaction taking place in the fermentation batch reactor. Most is purged to the absorption column which recovers ethanol, and the scrubbing water is recycled to the slurry tank. Beer Degasser Drum The remainder of the CO2 produced from fermentation is expunged by heating the beer. Distillation (Blue Section) Stripping Column Page 30 Department of Chemical Engineering University of Illinois at Chicago The fermentation broth is split into two streams. One stream is sent to this column operating at bar. Stripping Column The fermentation broth is split into two streams. One stream is sent to this column operating at .4 bar. Rectifying Column The product resulting from the stripping columns are 50% ethanol by weight and sent to the rectifying column at 5 bar. This produces ethanol at 92 wt% purity. Condensing heat of this column supplies energy to the reboiler of the bar stripping column. Molecular Sieve This produces anhydrous ethanol at fuel grade purity: wt%. Byproduct Processing (Purple Section) Centrifuge Non-fermentable products of the feed (whole stillage) consists of suspended grain solids, dissolved materials, and water. Whole stillage is sent to a centrifuge, where a wet cake (35% of solids by weight) and thin stillage (8% of solids by weight) are obtained. Part of the thin stillage is recycled (backset), and the rest is sent to an evaporator for further processing, which is out of the scope of our report. Page 31 Department of Chemical Engineering University of Illinois at Chicago References 1. Joern, Ernst, and Haldor Topsoee. “Ethyl and Isopropyl Alcohol.” SciFinder, Ger. Offen Patent CODEN:GWXXBX, , dfknj.wz.cz /view/scifinder/dfknj.wz.cz 2. Arpe, Hans-JuÌˆrgen, and Klaus Weissermel. Industrial Organic Chemistry. 3rd ed., Wiley-VCH, , dfknj.wz.cz _as/[Klaus_Weissermel,_Hans-Jurgen_Arpe]_Industrial_Or(dfknj.wz.cz).pdf. 3. K, Sam K. “Industrial Alcohol Production from Ethylene and Sulphuric Acid.” Inclusive Science and Engineering, Inclusive Science and Engineering: Science, Engineering & Technology for Business, Research, and Industries, 1 Apr. , dfknj.wz.czive dfknj.wz.cz d/. 4. Giada Franceschin, Andrea Zamboni, Fabrizio Bezzo, Alberto Bertucco, Ethanol from corn: a technical and economical assessment based on different scenarios, In Chemical Engineering Research and Design, Volume 86, Issue 5, , Pages , ISSN , dfknj.wz.cz 5. Marquez, Patricia Batre. “U.S. Ethanol: Production, Consumption, and the Relevance of Increasing Exports.” Ag Marketing Resource Center, Decision Innovation Solutions, 31 Mar. , dfknj.wz.cz 6. “U.S. Energy Information Administration - EIA - Independent Statistics and Analysis.” Growth Slows in U.S. Ethanol Production and Consumption - Today in Energy - U.S. Energy Information Administration (EIA), U.S. Energy Information Administration, 11 Sept. , dfknj.wz.cz?id= 7. O’Brien, Daniel, and Mike Woolverton. “The Relationship of Ethanol, Gasoline and Oil Prices.”Ag Marketing Resource Center, AgMRC Renewable Energy , 8 July , dfknj.wz.cz 8. Clifford, Caroline Burgess. “ How Corn Is Processed to Make Ethanol.” How Corn Is Processed to Make Ethanol | EGEE The Pennsylvania State University, dfknj.wz.cz 9. Todaro, Celeste M, and Henry C Vogel. “Fermentation and Biochemical Engineering Handbook.” Google Books, Elsevier Inc., , dfknj.wz.cz? id=PY_nAQAAQBAJ&lpg=PA71&dq=ethanol%2Bdry%2Bmill %2Bprocess&pg=PA71#v=onepage&q=ethanol%20dry%20mill%20process&f=false. Page 32 Department of Chemical Engineering University of Illinois at Chicago Clifford, Caroline Burgess. “ Composition of Corn and Yield of Ethanol from Corn.” Composition of Corn and Yield of Ethanol from Corn | EGEE Pennsylvania State University, dfknj.wz.cz “ Ethanol Industry Outlook.” Building Partnerships Growing Markets, , pp. 2–, dfknj.wz.cz Clean Cities. “Maps and Data.” Alternative Fuels Data Center: Maps and Data, U.S. Department of Energy, Jan. , dfknj.wz.cz Berkowitz, Justin, and Csaba Csere. “The CAFE Numbers Game: Making Sense of the New Fuel-Economy Regulations - Feature.” Car and Driver, Hearst Communications, Inc., Nov. , dfknj.wz.cz Gustafson, Cole, and Jason Fewell. “North Dakota State University.” Ethanol Production Dry versus Wet Grind Processing, North Dakota State University, , dfknj.wz.cz “U.S. Energy Information Administration.” How Much Ethanol Is in Gasoline, and How Does It Affect Fuel Economy? - FAQ - U.S. Energy Information Administration (EIA), 29 Mar. , dfknj.wz.cz?id=27&t= “Corn Milling: Wet vs. Dry.” Corn Milling | Wet vs. Dry | AMG Engineering, 13 Nov. , dfknj.wz.cz Franceschin, Giada, et al. “Ethanol from Corn: a Technical and Economical Assessment Based on Different Scenarios.” Chemical Engineering Research and Design, Elsevier B.V., 4 Mar. , dfknj.wz.cz? _rdoc=1&_fmt=high&_origin=gateway&_docanchor=&md5=bccfc9ca5f9 aeaa92ffb. 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MNGN - Introduction to Rock Mechanics
Fall Semester - Course Outline
Instructor:Dr. Ugur Ozbay
Office: BB ;tel: () ;email: email@example.com
The course aims at students developing a good working understanding of the basic and fundamental principles of rock mechanics as applied to designing and stabilizing excavations in rock masses.
Rock mechanics is fundamental to a wide variety of geo-science/engineering disciplines, the major ones being mining, civil, geology, geophysics, and dfknj.wz.cz is structured around the objective of students from mining and other geo-engineering branches developing a sound understanding of basic principles of rock dfknj.wz.czations of these principles to designing safe and economical structures in rock masses are also covered at an introductory level.
The course starts with introducing the concepts of stress, infinitesimal strain, and linear elasticity, which are the fundamentals to learning rock mechanics dfknj.wz.cz objective here is also to provide a basis for formulating the loading and deformation processes that take place in rock dfknj.wz.cz second section deals with failure of rock and rock dfknj.wz.cz laboratory classes on rock testing are supplementary to these first two dfknj.wz.cz should try to solve as many tutorial problems as you can to ensure that you are well equipped with a good knowledge of fundamental concepts to move on to the practice related subjects in the third and last section of the course.
The third section starts with describing rock mass as an engineering dfknj.wz.cz covers the methods of determining rock mass characteristics and classification dfknj.wz.cz distribution of stress and deformations in the rock mass surrounding excavations are dfknj.wz.czples of designing underground structures are explained using the simple example of a circular excavation developed in a hydrostatic stress dfknj.wz.cz excursions and in situ data collection exercises complement the subjects dealt with in this dfknj.wz.cz third section also includes dfknj.wz.cz subject of excavation support is dealt with at both fundamental and application dfknj.wz.cz stability analysis and design principles for rock slopes and mine pillars are discussed with the emphasis being on safety and dfknj.wz.czcal design exercises are carried out in the computer laboratory to help students to gain realistic insights to the rock engineering design processes.
You are responsible for knowing the material covered during lectures and laboratory dfknj.wz.cz are also responsible for the materials in the lecture notes, laboratory handouts, and the problems following each dfknj.wz.czg the material to be lectured before you come to class can help you greatly in understanding dfknj.wz.cz the completion of a module, assess yourself by returning to the module’s objectives to see whether you have achieved dfknj.wz.cz you feel that you have not accomplished the objectives, consult the references given or the books listed dfknj.wz.cz you are still unsure of any concept or require clarity or explanation, consult your TA or instructor.
Lecture material and books
A set of lecture notes will be available to the students at printing dfknj.wz.cz notes, by and large, are sufficient for following the dfknj.wz.czr, it is likely that you will need further clarification and details than covered by the lecture notes and if that happens to be the case then you are advised to refer to the notes by E Hoek at the web site dfknj.wz.cz or to buy the textbook Rock Mechanics for Underground Miningby B H G Brady and E T Brown, 2nd Edition, George Chapman and dfknj.wz.cz books that could be useful and are kept at the library are Rock Slope Engineering by E Hoek and J W Bray (2nd Edition).The book Fundamentals of Rock Mechanics by Jaeger and Cook, 3rd Edition is a “classic” that you may want to have it in your library if you are planning practicing rock mechanics/engineering.
Homework and Labs
There are about ten homework assignments and ten laboratory reports to be dfknj.wz.cz reports for these are due the next weekday after they are assigned and will be graded out of Late assignments will be graded out of 10 marks, if submitted within week of due dfknj.wz.cz homework will be accepted one week before a midterm date as the solutions to homework problems are published at the MNGN web dfknj.wz.cz work submitted is expected to be of high standard in content, structure and dfknj.wz.cz written reports will not be accepted unless very special circumstances are dfknj.wz.cz studies are encouraged but only lab reports can be submitted as dfknj.wz.czcal homework and lab reports will not be graded.
There will be 2 Midterm exams and a final exam, all in Classroom BBMidterm exam duration is normally one hour, although one and half midterm exams can also be dfknj.wz.cz exam covers the sections since the last dfknj.wz.cz final exam is two hours and covers the entire course.
This year, the course has started using BlackBoard for easier communication between the students and instructors. Go to the web site dfknj.wz.cz to see if you are registered for the "Introductory Rock Mechanics" site. The answers to the homework assignments and exam questions are published through BlackBoard. You should check the Blackboard utility also for announcements and other course related administrative issues such as details of modifications to field trips, laboratory classes, and lectures.
2 Midterms (each )
A ³ > B ³> C ³ > D ³ > F
The course schedule is published at dfknj.wz.cz